CN108439566A - A kind of mine system engineering flocculant and preparation method thereof - Google Patents

A kind of mine system engineering flocculant and preparation method thereof Download PDF

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CN108439566A
CN108439566A CN201810303964.1A CN201810303964A CN108439566A CN 108439566 A CN108439566 A CN 108439566A CN 201810303964 A CN201810303964 A CN 201810303964A CN 108439566 A CN108439566 A CN 108439566A
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parts
added
flocculant
reaction
melamines
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韦明
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Nanning Xiayang Chemical Technology Co Ltd
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Nanning Xiayang Chemical Technology Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/50Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/02Odour removal or prevention of malodour

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention belongs to sewage disposal processing technique field, specifically a kind of mine system engineering flocculation agent and preparation method thereof.Each constituent of the flocculant and its weight part ratio are:20 ~ 30 parts of butyl xanthates, 50 ~ 60 parts of melamines, 25 ~ 35 parts of ferrous sulfate, 20 ~ 25 parts of bentonites, 10 ~ 15 parts of Dry Flo PCs, 12 ~ 18 parts of polyvinylpyrrolidones, 10 ~ 16 parts of itaconic acid copolymers, 8 ~ 10 parts of fungicide, 100 ~ 150 parts of deionized waters.The mine system engineering preparation method of the present invention is first to be modified to melamine, then be mixed with to obtain the product of the present invention with other raw materials.The flocculant is nontoxic, and the flocculating setting time is short, high treating effect, and stability is high, will not cause secondary pollution.

Description

A kind of mine system engineering flocculant and preparation method thereof
Technical field
The invention belongs to sewage disposal processing technique field, specifically a kind of mine system engineering flocculation agent and its preparation side Method.
Background technology
With the development of the social economy, people increasingly increase the exploitation of mineral resources.Due to not conforming to mine resources The exploitation of reason causes to cause a degree of destruction, mine system engineering to ecological environment around mine to be primary pollution source therein One of.Mine system engineering is the various waste water generated during mining, have natural lixiviation water in mine, beneficiation wastewater, The leaching water etc. of rejects overflow water and slag stack-up-yard.In mine wastewater main pollutant component include organic pollution, Oil pollutant, soda acid pollutant, cyanide, heavy metal contaminants and solubility salt etc..Mine system engineering have discharge capacity it is big, The features such as, turbidity more containing mud is high, complicated component and water quality are unstable, it is unable to direct circulation utilization, if being discharged into river, lake In, water quality will be caused to change, kill or suppress growth of microorganism, interfere the self-purification of water, the heavy metal ion that sewage contains Soil can be also poisoned, Plant death is caused.During mining, the pollution control of mine wastewater is to have to asking for consideration Topic.
There are neutralisation, coagulation sedimentation, microbial method, artificial swamp method etc. to mine system engineering processing method at present.(1) in And method.Neutralisation is to put into alkali nertralizer in oxytropism waste water, changes the pH value of waste water using acid-base neutralization reaction, and makes a huge sum of money Belong to reacting with hydroxide ion and generate the heavy metal hydroxide of indissoluble, to have the function that removal.Neutralisation processing It is simple for process, it is easy to operate, but easily fouling, precipitating sludge amount are greatly, easily cause secondary pollution.(2) flocculation sedimentation.Flocculation is heavy Drop method is that flocculant is put into waste water to destroy the stability of colloid, and coacervation is settled at bulky grain to the metal in sewage The pollutant removals such as ion.(3) bioanalysis.Bioanalysis is by phase between biologic artifact or its metabolite and metal ion Interaction achievees the purpose that purification.Microbial method treated sewage is adaptable, at low cost, non-secondary pollution.(4) artificial swamp Method is Artificial Simulated Ecosystem, and the purification to sewage is realized using the method for ecology.Artificial swamp small investment, treatment effect Good, expense is low, but takes up a large area, larger by such environmental effects.
Flocculant is a kind of most common method in water technology.Flocculant is mainly with just(It is negative) electrical base It carries and is born (just in group and water)Electrical some particles for being difficult to detach or particle are close to each other, reduce its potential, make at its In unstable state, and using its aggregation property these particles are concentrated, and are separated by physics or chemical method, To reach the requirement of discharge.
Chinese patent 201210192293.9 discloses a kind of flocculant of sewage disposal.The flocculant material composition packet It includes:Starch, polyacrylamide, sodium hypochlorite, sodium carboxymethylcellulose, sodium metasilicate, potassium peroxydisulfate, sodium sulfite and water.Then Raw material is by the product that is combined.The flocculant made from the invention has environmentally protective, at low cost and adding less, wadding Solidifying speed is fast, and sludge is few;The advantages that easy to use, safe.
Chinese patent 201410348354.5 discloses a kind of level-one materialization intensive treatment coagulant of chemical engineering sewage, the wadding Solidifying agent is made of the raw material of following weight:Ferric sulfate 10-18kg, polymer aluminium silicate 8-12kg, sodium lignin sulfonate 4-9kg, carbon Nanotube 3-7kg, nano zine oxide 5-8kg, activated carbon fibre 3-6kg, polyvinyl alcohol 2-5kg, organo montmorillonite 2-5kg, phenol Urea formaldehyde 3-8kg, rapeseed oil 1-4kg, gas-produced black 1.5-3kg, propolis 0.5-2kg, calcium stearate 2-5kg, iron powder 8-12kg. The invention utilizes carbon nanotube, nano zine oxide, activated carbon fibre and other a variety of materialization reagent Combined Treatment chemical engineering sewages.
Chinese patent 201610462430.4 discloses a kind of sewage flocculant and preparation method thereof, the sewage flocculant by The raw material of following weight parts is made:1~5 part of sodium metasilicate, 1~5 part of magnesium chloride, 5~10 parts of ethyl alcohol, 1~5 part of polyacrylamide, 1~5 part of titanium tetrachloride, 0.1~0.5 part of diatomite, 1~5 part of aluminum sulfate, 10~20 parts of water, 0.1~0.5 part of hydrochloric acid.The sewage The preparation method of flocculant, steps are as follows:1) sodium metasilicate is proportionally mixed with magnesium chloride, it is equal that ethyl alcohol stirring is then added It is even;2) polyacrylamide, titanium tetrachloride, diatomite and aluminum sulfate co-grinding are added water uniformly mixed at powdered;3) will The product mixing that step 1) and step 2) obtain, while being continuously added hydrochloric acid and stirring evenly.The flocculant of the invention matches Science is prepared simply, easy to use, organic pollution and suspended matter in water can be effectively removed, to promote water process energy Power improves the quality of processing water.
The flocculant for being used for sewage disposal in the prior art has certain clean-up effect to sewage, but can have processing Effect is general, and usage amount is big, and settling velocity is slow, generates secondary pollution problems, or even can cause environmental pollution and to human body Health causes damages.
Invention content
The present invention provides a kind of mine system engineering flocculants and preparation method thereof, and the flocculant is nontoxic, flocculating setting Time is short, high treating effect, and stability is high, will not cause secondary pollution.
The scheme of the invention is realize in this way:A kind of mine system engineering flocculant, each constituent of the flocculant and Its weight part ratio is:20 ~ 30 parts of butyl xanthates, 50 ~ 60 parts of modified cyanurotriamides, 25 ~ 35 parts of ferrous sulfate, 20 ~ 25 parts it is swollen Moisten soil, 10 ~ 15 parts of Dry Flo PCs, 12 ~ 18 parts of polyvinylpyrrolidones, 10 ~ 16 parts of itaconic acid copolymers, 8 ~ 10 Part fungicide, 100 ~ 150 parts of deionized waters.
As further limiting for the present invention, the fungicide is BK fungicide, BIT fungicide according to 1:1 ratio Volume mixes.
A method of mine system engineering flocculant being prepared, preparation method step includes:
The preparation of step 1) modified cyanurotriamide:50 ~ 60 parts of melamines are divided into the trimerization that 3 parts of parts by weight are 18 ~ 20 parts Cyanamide;Then 5 ~ 6 parts of formaldehyde and 20 ~ 30 parts of ethylene glycol are added in three-necked flask, pH is adjusted to 8, while stirring with triethanolamine It mixes side and is warming up to 60 ~ 65 DEG C, 18 ~ 20 parts of melamines are then first added, be warming up to 75 ~ 80 DEG C, react 35 ~ 40min, add 18 ~ 20 parts of melamines, continue to react, and react 60 ~ 70min, add 18 ~ 20 parts of melamines, isothermal reaction to water When number is 3.0,10% caprolactam is added, reacts 8 ~ 10min, is cooled to 60 ~ 65 DEG C, is slowly added to 5%H2O2, and continue with three Ethanol amine adjusts pH value to 8;Waiting for H2O2, the reaction was complete(Bubble-free generates i.e. in reaction solution)When, stop reaction, be cooled to 40 DEG C, 45 ~ 50 parts of aluminium polychlorides are added into reaction solution, are stirred reaction, up to modified cyanurotriamide after drying followed by aging;
Step 2) hybrid reaction:Take 20 ~ 30 parts of butyl xanthates, 50 ~ 60 parts of modified cyanurotriamides, 25 ~ 35 parts of ferrous sulfate, 20 ~ 25 parts of bentonites, 10 ~ 15 parts of Dry Flo PCs, 12 ~ 18 parts of polyvinylpyrrolidones, 10 ~ 16 parts of itaconic acid copolymerization Object is added in 100 ~ 150 parts of deionized waters, is mixed evenly, and mixing speed is 200 ~ 300r/min, is spray-dried Fungicide is added afterwards to be uniformly mixed up to mine system engineering flocculant.
The technical principle that the present invention realizes is:
Butyl xanthate contains nonpolar base and polar group, and butyl xanthate, which is added, in flocculant can capture the Cu in sewage2+、 Zn2+、Ni2+Deng cation and tend to bonding and generate the butyl xanthate of indissoluble, to remove the heavy metal in sewage from Son, butyl xanthate can be used in room temperature and within the scope of very wide pH, and use scope is wide, and use condition is wide.
The flocculation of enhancing melamine is modified to melamine.Preparation three is modified to melamine first The reaction of melamine-formaldehyde resin, melamine and formaldehyde is reversible reaction, separates and melamine is added three times, can make trimerization Cyanamide is reacted with the free formaldehyde in reaction system, to promote reaction to forward and reverse movement, and then obtains lower free first The melamine resin of aldehyde reduces harm of the formaldehyde to environment.In addition being added separately to melamine can slow down instead The progress answered, there is the storage stability using melamine resin.Then again by aluminium polychloride to melamino-formaldehyde Resin is modified, and aluminium polychloride can play height charge neutrality and bridge linking effect, with melamine resin phase interaction With enhancing flocculant removes the effect of micro- noxious material and heavy metal ion, reduces flocculant usage, while can also enhance wadding Solidifying agent stability.Aluminium polychloride modified cyanurotriamide resin can also improve aluminium polychloride, and stability is poor in water, dispensing The problems such as amount is high, generates the shortcomings of flco is smaller and melamine resin Storage period is short, poorly water-soluble.
Ferrous sulfate can form colloid substance in water, impurity suspended matter that can be in absorption effluent, have good Flocculating effect, also has a good decoloring ability, heavy-metal ion removal, deoil, dephosphorization, the functions such as sterilization, so that sewage is reached Better clean-up effect.
Bentonite is nontoxic, it is tasteless, with larger specific surface area, have stronger cation exchange capacity (CEC);To various gases, Liquid, organic substance have certain adsorption capacity, can enhance suction-operated of the flocculant to pollutant, reduce flocculant and use Amount.
The addition of Dry Flo PC and polyvinylpyrrolidone has guarantor to the colloid that flocculant is formed in water Shield acts on, while can enhance the intermiscibility of flocculant in water, improves the flocculation sediment effect of flocculant.
Itaconic acid copolymer copolymer has efficient deodorization, being capable of ammonia, amine alkalinity malodorant and hydrogen sulfide etc. Acid malodorant reaction, reduces the foul smell of sewage, plays preferably purification sewage effect, while polymerization of itaconic acid object is with good Good biodegradability, is conducive to environmental protection.
BK fungicide has the function of quick sterilization, can quickly kill the bacterium in sewage, slow down the speed of bacterial reproduction, Reduce mine system engineering foul smell.BIT fungicide be a kind of wide spectrum, efficiently, the fungicide of low toxicity, good water solubility, the fungicide energy The microbial actions such as enough fungi, mould, bacterium and algae effectively inhibited in mine system engineering, promote formula compatibility strong.BK is killed Microbial inoculum and BIT fungicide are used in combination, and the effect to mine system engineering quick sterilization and long-acting bacteriostatic can be played, to the net of sewage Change is played the role of prodigious.
The present invention has following good result:
1. the flocculant of the present invention can use within the scope of very wide pH, temperature and dissolved oxygen amount need not be adjusted, it can be to mine Mountain sewage reaches good clean-up effect, adding less.
It can play the role of sterilization, deodorization, decoloration when 2. the flocculant of the present invention is while mine system engineering purifying, wad a quilt with cotton Solidifying agent is biodegradable or recycles, and will not cause secondary pollution.
3. the mine system engineering flocculant COD that the present invention is prepared is 20.9 ~ 23.5mg/L, COD removal rates >=98%, BOD For 5.8 ~ 7.1mg/L, BOD removal rate >=98%, heavy metal ion content is 0.87 ~ 1.09%, removal of heavy metal ions rate >= 98%, suspension content is 2.6 ~ 3.2mg/L, and fecal coliform group's number is 30 ~ 36MPN/L, and the flocculant properties are good, energy The harmful substance in mine system engineering is enough effectively removed, it is highly practical.
Specific implementation mode
A kind of mine system engineering flocculant of the description present invention and preparation method thereof with reference to embodiments, these descriptions are not The content of present invention is further limited.
Embodiment 1
50 ~ 60 parts of melamines are divided into 3 parts, first part of melamine parts by weight is 20 parts, second part of melamine weight Number is 18 parts, and third part melamine parts by weight are 18 parts;
The preparation of modified cyanurotriamide:6 parts of formaldehyde and 28 parts of ethylene glycol are added in three-necked flask, pH is adjusted with triethanolamine To 8, then 20 parts of melamines are first added to 64 DEG C in warming while stirring, be warming up to 80 DEG C, react 37min, add 18 parts Melamine continues to react, and reacts 60min, adds 18 parts of melamines, when isothermal reaction to water number is 3.0, is added 10% caprolactam reacts 8min, is cooled to 62 DEG C, is slowly added to 5%H2O2, and continue to adjust pH value to 8 with triethanolamine;It waits for The reaction was complete by H2O2(Bubble-free generates i.e. in reaction solution)When, stop reaction, be cooled to 40 DEG C, 45 parts are added into reaction solution and gathers Aluminium chloride is closed, reaction is stirred, up to modified cyanurotriamide after drying followed by aging;
Hybrid reaction:Take 20 parts of butyl xanthates, 50 parts of modified cyanurotriamides, 30 parts of ferrous sulfate, 24 parts of bentonites, 10 parts of octenes Base butanedioic acid aluminium starch, 18 parts of polyvinylpyrrolidones, 12 parts of itaconic acid copolymers are added in 100 parts of deionized waters, mixing It stirs evenly, mixing speed 250r/min, fungicide is added after being spray-dried and is uniformly mixed and flocculates up to mine system engineering Agent.
Embodiment 2
50 ~ 60 parts of melamines are divided into 3 parts, first part of melamine parts by weight is 19 parts, second part of melamine weight Number is 20 parts, and third part melamine parts by weight are 20 parts;
The preparation of modified cyanurotriamide:5 parts of formaldehyde and 30 parts of ethylene glycol are added in three-necked flask, pH is adjusted with triethanolamine To 8, then 19 parts of melamines are first added to 63 DEG C in warming while stirring, be warming up to 75 DEG C, react 35min, add 20 parts Melamine continues to react, and reacts 70min, adds 20 parts of melamines, when isothermal reaction to water number is 3.0, is added 10% caprolactam reacts 10min, is cooled to 65 DEG C, is slowly added to 5%H2O2, and continues to adjust pH value to 8 with triethanolamine; Waiting for H2O2, the reaction was complete(Bubble-free generates i.e. in reaction solution)When, stop reaction, be cooled to 40 DEG C, 50 parts are added into reaction solution Aluminium polychloride is stirred reaction, up to modified cyanurotriamide after drying followed by aging;
Hybrid reaction:Take 25 parts of butyl xanthates, 58 parts of modified cyanurotriamides, 32 parts of ferrous sulfate, 21 parts of bentonites, 14 parts of octenes Base butanedioic acid aluminium starch, 15 parts of polyvinylpyrrolidones, 15 parts of itaconic acid copolymers are added in 120 parts of deionized waters, mixing It stirs evenly, mixing speed 280r/min, fungicide is added after being spray-dried and is uniformly mixed and flocculates up to mine system engineering Agent.
Embodiment 3
50 ~ 60 parts of melamines are divided into 3 parts, first part of melamine parts by weight is 20 parts, second part of melamine weight Number is 18 parts, and third part melamine parts by weight are 20 parts;
The preparation of modified cyanurotriamide:5.5 parts of formaldehyde and 20 parts of ethylene glycol are added in three-necked flask, are adjusted with triethanolamine Then pH to 8, warming while stirring are first added 20 parts of melamines to 65 DEG C, are warming up to 76 DEG C, react 40min, add 18 Part melamine, continues to react, and reacts 65min, adds 20 parts of melamines and adds when isothermal reaction to water number is 3.0 Enter 10% caprolactam, react 9min, be cooled to 63 DEG C, be slowly added to 5%H2O2, and continues to adjust pH value to 8 with triethanolamine; Waiting for H2O2, the reaction was complete(Bubble-free generates i.e. in reaction solution)When, stop reaction, be cooled to 40 DEG C, 48 parts are added into reaction solution Aluminium polychloride is stirred reaction, up to modified cyanurotriamide after drying followed by aging;
Hybrid reaction:Take 30 parts of butyl xanthates, 60 parts of modified cyanurotriamides, 25 parts of ferrous sulfate, 23 parts of bentonites, 15 parts of octenes Base butanedioic acid aluminium starch, 17 parts of polyvinylpyrrolidones, 10 parts of itaconic acid copolymers are added in 150 parts of deionized waters, mixing It stirs evenly, mixing speed 300r/min, fungicide is added after being spray-dried and is uniformly mixed and flocculates up to mine system engineering Agent.
Embodiment 4
50 ~ 60 parts of melamines are divided into 3 parts, first part of melamine parts by weight is 18 parts, second part of melamine weight Number is 20 parts, and third part melamine parts by weight are 18 parts;
The preparation of modified cyanurotriamide:5.2 parts of formaldehyde and 25 parts of ethylene glycol are added in three-necked flask, are adjusted with triethanolamine Then pH to 8, warming while stirring are first added 18 parts of melamines to 60 DEG C, are warming up to 77 DEG C, react 38min, add 20 Part melamine, continues to react, and reacts 63min, adds 18 parts of melamines and adds when isothermal reaction to water number is 3.0 Enter 10% caprolactam, react 8.5min, be cooled to 60 DEG C, be slowly added to 5%H2O2, and continue with triethanolamine adjust pH value to 8;Waiting for H2O2, the reaction was complete(Bubble-free generates i.e. in reaction solution)When, stop reaction, is cooled to 40 DEG C, 49 are added into reaction solution Part aluminium polychloride, is stirred reaction, up to modified cyanurotriamide after drying followed by aging;
Hybrid reaction:Take 28 parts of butyl xanthates, 52 parts of modified cyanurotriamides, 28 parts of ferrous sulfate, 20 parts of bentonites, 12 parts of octenes Base butanedioic acid aluminium starch, 12 parts of polyvinylpyrrolidones, 13 parts of itaconic acid copolymers are added in 140 parts of deionized waters, mixing It stirs evenly, mixing speed 230r/min, fungicide is added after being spray-dried and is uniformly mixed and flocculates up to mine system engineering Agent.
Embodiment 5
50 ~ 60 parts of melamines are divided into 3 parts, first part of melamine parts by weight is 18 parts, second part of melamine weight Number is 19 parts, and third part melamine parts by weight are 19 parts;
The preparation of modified cyanurotriamide:5.8 parts of formaldehyde and 22 parts of ethylene glycol are added in three-necked flask, are adjusted with triethanolamine Then pH to 8, warming while stirring are first added 18 parts of melamines to 61 DEG C, are warming up to 78 DEG C, react 36min, add 19 Part melamine, continues to react, and reacts 68min, adds 19 parts of melamines and adds when isothermal reaction to water number is 3.0 Enter 10% caprolactam, react 9.5min, be cooled to 64 DEG C, be slowly added to 5%H2O2, and continue with triethanolamine adjust pH value to 8;Waiting for H2O2, the reaction was complete(Bubble-free generates i.e. in reaction solution)When, stop reaction, is cooled to 40 DEG C, 47 are added into reaction solution Part aluminium polychloride, is stirred reaction, up to modified cyanurotriamide after drying followed by aging;
Hybrid reaction:Take 23 parts of butyl xanthates, 55 parts of modified cyanurotriamides, 35 parts of ferrous sulfate, 25 parts of bentonites, 13 parts of octenes Base butanedioic acid aluminium starch, 14 parts of polyvinylpyrrolidones, 16 parts of itaconic acid copolymers are added in 130 parts of deionized waters, mixing It stirs evenly, mixing speed 200r/min, fungicide is added after being spray-dried and is uniformly mixed and flocculates up to mine system engineering Agent.
The flocculant that the embodiment of the present invention is prepared is pair for mine system engineering processing, and with commercially available flocculant Product carry out properties of product test in the same old way, and the performance test results are as shown in table 1 below.
1 flocculant product performance of table
The above embodiment of the present invention scheme is only the description of the invention and cannot limit the present invention, this is indicated in claim The range of invention product form ingredient, component ratio, preparation method parameter, and above-mentioned explanation does not point out parameter of the present invention Range, therefore, any change within the meaning and scope equivalent to the claims of the present invention, be all considered to be including In the range of claims.
The present invention is and to pass through creative work by multidigit mine system engineering treatment technology personnel's long-term work experience accumulation It creates.The mine system engineering flocculant properties of the present invention are good, can effectively remove the harmful substance in mine system engineering, make Sewage can be utilized effectively after treatment, reduce environmental pollution, disclosure satisfy that industry requirement, before having preferable application Scape.

Claims (2)

1. a kind of mine system engineering flocculant, characterized in that each constituent of the flocculant and its weight part ratio are:20 ~ 30 parts Butyl xanthate, 50 ~ 60 parts of melamines, 25 ~ 35 parts of ferrous sulfate, 20 ~ 25 parts of bentonites, 10 ~ 15 parts of ocentyl succinic aluminium Starch, 12 ~ 18 parts of polyvinylpyrrolidones, 10 ~ 16 parts of itaconic acid copolymers, 8 ~ 10 parts of fungicide, 100 ~ 150 parts of deionizations Water;
The fungicide is BK fungicide, BIT fungicide according to 1:1 ratio volume mixes.
2. a kind of method preparing mine system engineering flocculant as described in claim 1, characterized in that preparation method step packet It includes:
The preparation of step 1) modified cyanurotriamide:50 ~ 60 parts of melamines are divided into the trimerization that 3 parts of parts by weight are 18 ~ 20 parts Cyanamide;Then 5 ~ 6 parts of formaldehyde and 20 ~ 30 parts of ethylene glycol are added in three-necked flask, pH is adjusted to 8, while stirring with triethanolamine It mixes side and is warming up to 60 ~ 65 DEG C, 18 ~ 20 parts of melamines are then first added, be warming up to 75 ~ 80 DEG C, react 35 ~ 40min, add 18 ~ 20 parts of melamines, continue to react, and react 60 ~ 70min, add 18 ~ 20 parts of melamines, isothermal reaction to water When number is 3.0,10% caprolactam is added, reacts 8 ~ 10min, is cooled to 60 ~ 65 DEG C, is slowly added to 5%H2O2, and continue with three Ethanol amine adjusts pH value to 8;Wait for H2O2The reaction was complete(Bubble-free generates i.e. in reaction solution)When, stop reaction, be cooled to 40 DEG C, 45 ~ 50 parts of aluminium polychlorides are added into reaction solution, are stirred reaction, up to modified cyanurotriamide after drying followed by aging;
Step 2) hybrid reaction:Take 20 ~ 30 parts of butyl xanthates, modified cyanurotriamide, 25 ~ 35 parts of ferrous sulfate, 20 ~ 25 parts of swellings Soil, 10 ~ 15 parts of Dry Flo PCs, 12 ~ 18 parts of polyvinylpyrrolidones, 10 ~ 16 parts of itaconic acid copolymers are added to It in 100 ~ 150 parts of deionized waters, is mixed evenly, mixing speed is 200 ~ 300r/min, is added and kills after being spray-dried Microbial inoculum is uniformly mixed up to mine system engineering flocculant.
CN201810303964.1A 2018-04-08 2018-04-08 A kind of mine system engineering flocculant and preparation method thereof Pending CN108439566A (en)

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CN111039375A (en) * 2019-12-23 2020-04-21 中冶京诚工程技术有限公司 Flocculating agent for mine beneficiation wastewater treatment and preparation method and application thereof
CN111807489A (en) * 2020-08-06 2020-10-23 中科乐美环保科技有限公司 Composite flocculant for urban sewage treatment and use method thereof

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Application publication date: 20180824